US3768290A - Method of modifying a finned tube for boiling enhancement - Google Patents

Method of modifying a finned tube for boiling enhancement Download PDF

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US3768290A
US3768290A US00154312A US3768290DA US3768290A US 3768290 A US3768290 A US 3768290A US 00154312 A US00154312 A US 00154312A US 3768290D A US3768290D A US 3768290DA US 3768290 A US3768290 A US 3768290A
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fin
inch
gap
convolutions
fins
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V Zatell
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Bank of Nova Scotia
Wolverine Tube Inc
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UOP LLC
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/18Arrangements for modifying heat-transfer, e.g. increasing, decreasing by applying coatings, e.g. radiation-absorbing, radiation-reflecting; by surface treatment, e.g. polishing
    • F28F13/185Heat-exchange surfaces provided with microstructures or with porous coatings
    • F28F13/187Heat-exchange surfaces provided with microstructures or with porous coatings especially adapted for evaporator surfaces or condenser surfaces, e.g. with nucleation sites
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B21MECHANICAL METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
    • B21CMANUFACTURE OF METAL SHEETS, WIRE, RODS, TUBES OR PROFILES, OTHERWISE THAN BY ROLLING; AUXILIARY OPERATIONS USED IN CONNECTION WITH METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL
    • B21C37/00Manufacture of metal sheets, bars, wire, tubes or like semi-manufactured products, not otherwise provided for; Manufacture of tubes of special shape
    • B21C37/06Manufacture of metal sheets, bars, wire, tubes or like semi-manufactured products, not otherwise provided for; Manufacture of tubes of special shape of tubes or metal hoses; Combined procedures for making tubes, e.g. for making multi-wall tubes
    • B21C37/15Making tubes of special shape; Making tube fittings
    • B21C37/20Making helical or similar guides in or on tubes without removing material, e.g. by drawing same over mandrels, by pushing same through dies ; Making tubes with angled walls, ribbed tubes and tubes with decorated walls
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T29/00Metal working
    • Y10T29/49Method of mechanical manufacture
    • Y10T29/4935Heat exchanger or boiler making
    • Y10T29/49377Tube with heat transfer means
    • Y10T29/49378Finned tube
    • Y10T29/49382Helically finned
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T29/00Metal working
    • Y10T29/49Method of mechanical manufacture
    • Y10T29/4935Heat exchanger or boiler making
    • Y10T29/49377Tube with heat transfer means
    • Y10T29/49378Finned tube
    • Y10T29/49385Made from unitary workpiece, i.e., no assembly

Definitions

  • the present disclosure relates to tubes in which heat transfer fins of usual shape are provided on the outer surface thereof. These fins may be separate annular fins or they may be provided to extend helically on the outer surface of the tube. In the latter case the fin convolutions may be in the form of a single helix or two or three or more separate but interleaved helical fins may be provided.
  • the fins are formed on the tube by well known processes such for example as disclosed in Locke U.S. Pat. No. 1,865,575.
  • the fins are integral with the material of the tube wall and are formed to extend outwardly from the tube wall by rolling operations.
  • each fin convolution extends substantially radially outwardly from the tube, whether provided in the form of single annular convolutions or a multiplicity of helical convolutions.
  • the fins are outwardly tapered and have a height which substantially exceeds the average fin thickness as well as the average spacing between adjacent fin convolutions.
  • these fins are bent or formed so that the crest of some or all of the fins is closely adjacent to the surface of the next adjacent fin convolution with the result that there is provided a confined space of substantial size having a port or passage leading outwardly therefrom defined between the tip of one fin convolution and the side of the next adjacent convolution.
  • This bending over of the fins may be accomplished in different ways, some of which are applicable to singlestart fins and others of which are designed for use with .different multiple-start fins.
  • the finned tubing is simply drawn through a die which is dimensioned to bend the fin convolutions over into required position. Best results have been obtained when the dimensions and configuration of the die is such that the crest of each fin convolution is not only bent over into contact with a surface of the next adjacent fin convolution, but is forced beyond the position of initial contact.
  • the bent over fins upon emergence from the die, spring back out of contact with the adjacent surface and remain at a predetermined substantially accurately controlled spacing therefrom.
  • the fins are reformed by rolls or dies during or subsequent to the finning operation.
  • the confined space is annular in shape.
  • the convolutions are in the form of a single-start fin extending helically from the tube, the confined space is in the form of a single elongated helically disposed space.
  • multiplehelix fins are provided, separate elongated helically disposed confined spaces result.
  • the closure provided by bending over the fins does not produce a perfectly accurate continuous gapbetween tee crests of the bent-over fin convolutions, but instead, theremay be some variation such for example as areas in which the fin tips remain in contact with the surface of the adjacent convolution and are spaced therefrom at varying intervals.
  • the control of the spacing may accordingly be considered as providing an average spacing rather than a perfectly accurate continuous spacing.
  • Tests of operating efficiency of the tubing modified for boiling enhancement indicate that the average width of the space or gap between the crests of a fin convolution and the adjacent surface of the next convolution should be up to 0.007 inch. The maximum improvement in boiling efficiency is noted where the gap does not exceed 0.005 inch.
  • FIG. 1 is an enlarged fragmentary section through a wall of a finned tube.
  • FIGS. 2-4 are sectional views showingthe configuration of fins bent over after passage through differently dimensioned dies.
  • FIG. 5 is a fragmentary sectional view illustrating a somewhat different embodiment of the disclosure.
  • FIGS. 6-9 are fragmentary sectional views illustrating fin configurations for double-finned or double-start finned tubing.
  • FIG. 10 is a fragmentary sectional view showing one embodiment of fin modification.
  • FIG. 11 is a view similar. to FIG. 10 showing another embodiment of the disclosure.
  • FIG. 12 is a graph showing comparative boiling efficiencies of a plain tube and a tube made in accordance with the present disclosure.
  • conventional integrally finned tubing is modified to enhance boiling by bending the tips of the fin convolutions over so that a small gap of controlled size is formed between the tip of one convolution and the side or other adjacent surface of the next fin convolution.
  • FIG. 1 there is shown in enlargement a fragmentary section through the wall of a finned tube provided with a multiplicity of fins 14 which may, for example, be separate and independent annular fins, or provided in helical arrangement with one or more separate helical fins.
  • the fin of the actual tube illustrated in FIG. 1 was a single helix; however, tubes shown in FIGS. 2, 3 and 4 could also be made from multiple-helix fin tube.
  • FIG. 2 there is illustrated the resulting deformation of the fin after the tube (which has an initial outside diameter of 0.740 inch) was drawn through a die of circular cross-section having an internal diameter of 0.695 inch.
  • the average space as indicated at 16, between' the crests of the fin convolution and the adjacent side surface of the next adjacent fin convolution was found to be 0.0035 0.0050 inch.
  • An inspection of this Figure indicates that there is thus provided a continuous substantially closed space or chamber 17 through which liquid in contact with the finned surface may enter. It will of course further be apparent that where the fins 14 are in the form of separate annular fins, these enclosed spaces or chambers 17 are annular and are equal in number to the number of fins.
  • the fin is provided in the form of a single helical fin, it will be apparent that the configuration illustrated in FIG. 2 results in a single helically extending enclosed space or chamber. Similarly, where two or three separate but interleaved helical fins are provided, the enclosed spaces or chambers are helical and are equal in number to the number of separate fins.
  • FIG. 3 there is illustrated the fin configuration when the same finned tube shown in FIG. 1 was drawn through a die having an internal diameter of 0.688 inch.
  • the gap between the crests of the fin convolutions and the adjacent side surface of the next adjacent convolution was found to have an average width of 0.0020 0.0045 inch.
  • the location of the gap or gaps is indicated at 18.
  • the tube formation illustrated results in the essentially enclosed space or chamber 19 which may be circular or helical as described in connection with FIG. 2.
  • FIG. 4 there is illustrated the fin configuration when the same tube is drawn through a die having an internal diameter of 0.675 inch.
  • the crests of the fin convolution were bent over and deformed the material of the adjacent convolution as indicated at 21, so that no gap was visible to the unaided eye.
  • a reproducible finite gap is visible when microscopically examined.
  • Tubing having the configuration illustrated in FIGS. 2, 3 and 4 has been subjected to boiling tests and it has been found that for substantial enhancement of boiling, the gap into the enclosed annular or helical space should have an average width of 0.007 inch or less with the maximum improvement occurring where the gap is 0.005 inch or less.
  • variable parameters which influence the efficiency of the disclosed construction in enhancing boiling are number of fins per inch of tubing and gap to trapped volume ratio, as well as gap width.
  • the number of fins per F l1WillP9L ljl9- Tubing generally of the type illustrated in FIGS. 2, 3 and 4 was subjected to boiling tests in which boiling A T (which for this purpose may be considered as the difference between the average temperature of the tube wall metal and the boiling temperature of the fluid outside the tube) was determined for different heat flux values based on outside area BTU/Hr-Ft.
  • the l9-fin tubing having the fins bent over to define restricted substantially enclosed spaces represents an improvement over the unmodified finned tube in the required A T of about 54 percent.
  • modified 26-fin tubing showed an improvement of about percent in the boiling A T over unmodified tubing.
  • FIG. 12 graphically illustrates the enhancement in boiling which follows bending or forming the fins of a 26-fin tube, such as seen in FIG. 1, to the form shown in FIG. 3.
  • this tube where the gap between the crests of the fins and the side surface of the adjacent fin convolution has an average dimension of 0.002 0.045 inch. From this graph, it will be noted that at 6 feet per ton, the boiling AT for 26-fin standard tube is 12 F.
  • the finned tubing modified in accordance with the present invention is referred to as Z-fin tube, and for the 26 Z-fin tube illustrated in FIG. 3, the boiling AT is 2.5 F. for an improvement of about percent in the boiling film temperature drop. 7
  • FIG. 5 illustrates another fin configuration for a single helix tube when formed by a process other than drawing through a circular die.
  • this Figure no attempt is made to illustrate a gap between the crest portion of a finned convolution and the side of the next adjacent convolution, but it is to be understood that an average gap of less than 0.007 inch will be provided.
  • FIG. 6 there is illustrated a modified finned tube 24 produced from a double or twostart fin.
  • each of the fins 26 is inclined towards each other so that a gap of controlled dimensions is provided at 28 between the crests of the fins.
  • a helical substantially enclosed space or chamber 29 is formed.
  • the fins30 are bent toward each other in such a way as to define a gap 32 therebetween, this gap appearing between spaced apart fin portions which are relatively flat in cross-section.
  • the confined space 34 is essentially smaller than the space 29 provided between the fins in FIG. 6.
  • FIG. 8 an arrangement is illustrated in which one of the fins 36 is not modified and the other fin 38 is bent towards the unmodified fin as illustrated so as to produce the helical substantially enclosed space or chamber 40 and the controlled restricted gap or opening 42.
  • FIG. 9 there is illustrated an arrangement generally similar to that shown in FIG. 6 except that the separate fins 44 and 46 are curved and inclined towards each other to produce a substantially circular cross-section enclosed space or chamber 48 and the narrow restricted gap 50.
  • FIGS. and 11 The tubing of FIGS. and 11 is produced from finned tubing have three interleaved helical fins.
  • the fins 62 and 64 are illustrated as bent toward the intermediate unmodified fin 63 so as to define the substantially enclosed spaces or chambers 66.
  • the fins here designated 62a and 64a, are bent in a different manner toward the intermediate fin 63a to define the substantially enclosed spaces or chambers 66a.
  • the finned tube as illustrated in FIG. 1, prior to bending over the fins, has in a typical example the following dimensions:
  • the internal diameter of the tube is 0.557 inch and the wall thickness, measured from the inside of the tube to the bottom of the space between adjacent fins is 0.035 inch.
  • the fins have a radial dimension of 0.057 inch and are provided at a frequency of about 26 fins per inch, giving a pitch from fin convolution to fin convolution of approximately 0.038 inch.
  • the individual fins have a thickness at the base of approximately 0.0165 inch and at the tip or crest of 0.0075 inch. This gives an average width of approximately 0.012 inch.
  • the space between adjacent fins increases from approximately 0.021 inch adjacent the roots of the fins to approximately 0.0305 inch adjacent the crests.
  • the finned tubing illustrated in FIG. 1 has an approximate outside diameter, before the bending of the fins, of 0.740 inch.
  • FIG. 3 Theconfiguration illustrated in FIG. 3'results from drawing the tubing illustrated in FIG. 1 through a die having an internal diameter of 0.688 inch, which produced a gap 18 communicating with the space 19 of 0.002 0.004s inch.
  • FIG. 4 resulted from drawing the tubing of FIG. 1 through a die having an internal diameter of 0.675 inch. In this operation the crests of each fin convolution were bent over into con tact with the next adjacent fin convolution with such force as to provide deformation of the material, as has been previously described.
  • the dimensions of the fins in relationship to spacing are of course of critical nature since this determines the general shape and dimensions of space which is enclosed when the outer portion of each fin convolution is bent over into close proximity to the adjacent wall portion of the adjacent fin convolution, to provide the restricted opening into the substantially enclosed space.
  • the fin height should be greater than the spacing between adjacent fins and the fin tip thickness should be substantially less than the fin thickness at the root.
  • the height of the fin is substantially greater than the average width, as for example, not less than twice the average width.
  • the fins are formed by rolling up material from the outer wall of the tubing, so that the fins originally extend generally perpendicular to the surface from which they were displaced, and portions thereof extend generally parallel to corresponding portions of adjacent fin convolutions.
  • the average spacing between adjacent fin portions is greater than the average thickness of the fins. This results inherently in the production of substantially enclosed spaces or chambers, after the outer portions of the fins are bent over, which are of quite substantial size. At the same time, the openings into the substantially enclosed spaces may be very restricted, by bending the outer portions of tube convolutions into very close spacing from the side surface of adjacent fin portions.
  • the method of making tubing modified for the enhancement of boiling of liquid in contact with the exterior surface thereof which comprises rolling up fin convolutions out of the material at the exterior of the tubing with each convolution extending generally radially outwardly of the tubing parallel to and spaced substantially from adjacent convolutions, and thereafter drawing the finned tube through a die having a throat with a minimum transverse dimension smaller than the outside diameter of the original fin convolutions to form the outer portions of fin convolutions completely around the finned tube into proximity to a side of adjacent fin convolutions to define therewith a substantially enclosed space extending around the tubing and a restricted opening into such space.

Abstract

Tubing having circumferentially extending fins, either annular or helical, is modified by forming or bending the fins transversely so that the tip of each fin convolution is closely adjacent to a portion of the next adjacent fin convolution providing small continuous or discrete gaps of predetermined and controlled average size into substantially confined spaces between adjacent fin convolutions.

Description

United States Patent 1191 Zatell Oct. 30, 1973 METHOD OF MODIFYING A FINNED TUBE 3,454,081 7/1969 Kun et al. 165/133 FOR BOILING ENHANCEMENT 3,696,861 10/1972 Webb 3,696,863 10/1972 Sung Chul Kim l65/l8l X [75] Inventor: Vincent A. Zatell, Lathrup Village,
Mich FOREIGN PATENTS OR APPLICATIONS 1,533,025 7 1968 F 165 181 1 1 Assrgnw Products, Des 595,680 12/1947 61127811131" 165/184 22 Fil June 1 1971 Primary Examiner-Charles W. Lanham Assistant Examiner-D. C. Reiley, III [21] PP N04 154,312 Att0rneyCharles R. McKinley et al.
52 us. c1. 72/68, 29/1573 AH, 29/1573 B, [571 ABSTRACT 72/367, 165/133 Tubing having circumferentially extending fins, either [51] Int. Cl. B21b 15/00 nn l r r h li l, i m ifi y f rming r nding [58] Field of Search 29/1573 A, 157.3 AH, h fin r n v r ely so ha he ip f each fin c0nv0- 29/1573 B; 165/133, 181, 184; 72/68, 367 lution is closely adjacent to a portion of the next adjacent fin convolution providing small continuous or dis- [56] References Cited crete gaps of predetermined and controlled average UNITED STATES PATENTS size into substantially confined spaces between adja- 3,602,027 3 1971 Klug .1 29 1573 AH cent fin wnvOlunonS' 3,326,283 6/1967 Ware 165/184 X 16 Claims, 12 Drawing Figures Y//,. 695 0/5 0035' 005 64 '0 O0OI,,4I a 0,'0,
METHOD OF MODIFYING A FINNED TUBE FOR BOILING ENHANCEMENT BRIEF SUMMARY OF THE DISCLOSURE It hasbeen found that heat transfer tubes adapted to transfer heat from a fluid flowing within the tube to a liquid in contact with the outer surface of the tube for the purpose of boiling the liquid, have a substantially increased efficiency in boiling the liquid, when they are provided with a porous surface having a multiplicity of substantially confined spaces into which the liquid may flow. These spaces have substantially restricted ports or passages providing for flow of liquid into the spaces and for escape of vapor from the substantially confined spaces.
The present disclosure relates to tubes in which heat transfer fins of usual shape are provided on the outer surface thereof. These fins may be separate annular fins or they may be provided to extend helically on the outer surface of the tube. In the latter case the fin convolutions may be in the form of a single helix or two or three or more separate but interleaved helical fins may be provided.
Preferably, the fins are formed on the tube by well known processes such for example as disclosed in Locke U.S. Pat. No. 1,865,575. In finned tubing of this type the fins are integral with the material of the tube wall and are formed to extend outwardly from the tube wall by rolling operations. As initially produced, each fin convolution extends substantially radially outwardly from the tube, whether provided in the form of single annular convolutions or a multiplicity of helical convolutions. The fins are outwardly tapered and have a height which substantially exceeds the average fin thickness as well as the average spacing between adjacent fin convolutions.
In accordance with the present disclosure, these fins are bent or formed so that the crest of some or all of the fins is closely adjacent to the surface of the next adjacent fin convolution with the result that there is provided a confined space of substantial size having a port or passage leading outwardly therefrom defined between the tip of one fin convolution and the side of the next adjacent convolution.
This bending over of the finsmay be accomplished in different ways, some of which are applicable to singlestart fins and others of which are designed for use with .different multiple-start fins. In the simplest form of the invention the finned tubing is simply drawn through a die which is dimensioned to bend the fin convolutions over into required position. Best results have been obtained when the dimensions and configuration of the die is such that the crest of each fin convolution is not only bent over into contact with a surface of the next adjacent fin convolution, but is forced beyond the position of initial contact. When the die dimensions are properly controlled the bent over fins upon emergence from the die, spring back out of contact with the adjacent surface and remain at a predetermined substantially accurately controlled spacing therefrom. In other forms of the invention the fins are reformed by rolls or dies during or subsequent to the finning operation.
It will be appreciated that where the fins are in the form of annular convolutions, the confined space is annular in shape. Where the convolutions are in the form of a single-start fin extending helically from the tube, the confined space is in the form of a single elongated helically disposed space. Similarly, where multiplehelix fins are provided, separate elongated helically disposed confined spaces result.
It will further be appreciated that the closure provided by bending over the fins does not produce a perfectly accurate continuous gapbetween tee crests of the bent-over fin convolutions, but instead, theremay be some variation such for example as areas in which the fin tips remain in contact with the surface of the adjacent convolution and are spaced therefrom at varying intervals. The control of the spacing may accordingly be considered as providing an average spacing rather than a perfectly accurate continuous spacing.
Tests of operating efficiency of the tubing modified for boiling enhancement indicate that the average width of the space or gap between the crests of a fin convolution and the adjacent surface of the next convolution should be up to 0.007 inch. The maximum improvement in boiling efficiency is noted where the gap does not exceed 0.005 inch.
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is an enlarged fragmentary section through a wall of a finned tube.
FIGS. 2-4 are sectional views showingthe configuration of fins bent over after passage through differently dimensioned dies.
FIG. 5 is a fragmentary sectional view illustrating a somewhat different embodiment of the disclosure.
FIGS. 6-9 are fragmentary sectional views illustrating fin configurations for double-finned or double-start finned tubing.
FIG. 10 is a fragmentary sectional view showing one embodiment of fin modification.
FIG. 11 is a view similar. to FIG. 10 showing another embodiment of the disclosure.
FIG. 12 is a graph showing comparative boiling efficiencies of a plain tube and a tube made in accordance with the present disclosure.
DETAILED DESCRIPTION It has been found that porous finishes, points or small gaps leading to partially confined spaces generally enhance the boiling capacity of a surface. Recent examples of such enhancement noted in the patent literature are tip indented finned tubing shown in US. Pat No. 3,487,670, a wire wound finned tube shown in US. Pat. No. 3,521,708, and microscopically grooved surfaces shown in US. Pat. Nos. 3,454,081 and 3,496,752.
In accordance with the present invention, conventional integrally finned tubingis modified to enhance boiling by bending the tips of the fin convolutions over so that a small gap of controlled size is formed between the tip of one convolution and the side or other adjacent surface of the next fin convolution. From the foregoing it will be apparent that the small gap of controlled size leads to a substantially enlarged chamber or space which extends around the tube in the form of one or more convolutions depending upon whether the fins are initially annular or helical.
In the first place, it has been found that by methods which will subsequently be described, predictable small gaps up to 0.007 inch may be produced by a simple drawing operation of the finned tube through a die having a circular cross-section and dimensioned to bend the fin convolutions as required.
Further investigation has indicated that substantial improvement in boiling efficiency is obtained when the gaps as above described, have an average width up to 0.007 inch with the maximum improvement where gap widths are 0.005 inch or less.
While the simplest method of bending the fins to produce the required spacing is to draw the finned tube through the die, other methods are of course available and may be necessary when the procedure is applied to multiple-start fins in which different formation is imparted to the separate fins.
Referring now to FIG. 1, there is shown in enlargement a fragmentary section through the wall of a finned tube provided with a multiplicity of fins 14 which may, for example, be separate and independent annular fins, or provided in helical arrangement with one or more separate helical fins. The fin of the actual tube illustrated in FIG. 1 was a single helix; however, tubes shown in FIGS. 2, 3 and 4 could also be made from multiple-helix fin tube.
In FIG. 2 there is illustrated the resulting deformation of the fin after the tube (which has an initial outside diameter of 0.740 inch) was drawn through a die of circular cross-section having an internal diameter of 0.695 inch. The average space as indicated at 16, between' the crests of the fin convolution and the adjacent side surface of the next adjacent fin convolution was found to be 0.0035 0.0050 inch. An inspection of this Figure indicates that there is thus provided a continuous substantially closed space or chamber 17 through which liquid in contact with the finned surface may enter. It will of course further be apparent that where the fins 14 are in the form of separate annular fins, these enclosed spaces or chambers 17 are annular and are equal in number to the number of fins. Where the fin is provided in the form of a single helical fin, it will be apparent that the configuration illustrated in FIG. 2 results in a single helically extending enclosed space or chamber. Similarly, where two or three separate but interleaved helical fins are provided, the enclosed spaces or chambers are helical and are equal in number to the number of separate fins.
In FIG. 3 there is illustrated the fin configuration when the same finned tube shown in FIG. 1 was drawn through a die having an internal diameter of 0.688 inch. In this case the gap between the crests of the fin convolutions and the adjacent side surface of the next adjacent convolution was found to have an average width of 0.0020 0.0045 inch. In this Figure the location of the gap or gaps is indicated at 18. The tube formation illustrated results in the essentially enclosed space or chamber 19 which may be circular or helical as described in connection with FIG. 2.
In FIG. 4 there is illustrated the fin configuration when the same tube is drawn through a die having an internal diameter of 0.675 inch. In this case it was found that the crests of the fin convolution were bent over and deformed the material of the adjacent convolution as indicated at 21, so that no gap was visible to the unaided eye. However, a reproducible finite gap is visible when microscopically examined.
The three configurations of tube described in the foregoing are for the purpose of indicating that an accurate control of the average gap between te crests of the tube convolutions and the adjacent side wall of the adjacent convolution can be predetermined and maintained by selecting the appropriate die through which the finned tube is drawn.
Tubing having the configuration illustrated in FIGS. 2, 3 and 4 has been subjected to boiling tests and it has been found that for substantial enhancement of boiling, the gap into the enclosed annular or helical space should have an average width of 0.007 inch or less with the maximum improvement occurring where the gap is 0.005 inch or less.
The variable parameters which influence the efficiency of the disclosed construction in enhancing boiling are number of fins per inch of tubing and gap to trapped volume ratio, as well as gap width. In accordance with the present invention, the number of fins per F l1WillP9L ljl9- Tubing generally of the type illustrated in FIGS. 2, 3 and 4 was subjected to boiling tests in which boiling A T (which for this purpose may be considered as the difference between the average temperature of the tube wall metal and the boiling temperature of the fluid outside the tube) was determined for different heat flux values based on outside area BTU/Hr-Ft.
When the tubing was tested at 4,000 BTU/Hr-Ft, the test results were as tabulated:
fins/inch Average Gap A T l 19 0.001 0.0016" 53 F. 2 19 0.0035 0.0040" 53 F. 3 19 (standard fins) l l.5 F. 4 26 less than 0.001" 3.0 F. 5 26 0.002 0.0045" 3.0 F. 6 26 (standard fins) 120 F.
It is thus seen that the l9-fin tubing having the fins bent over to define restricted substantially enclosed spaces represents an improvement over the unmodified finned tube in the required A T of about 54 percent.
Similarly, the modified 26-fin tubing showed an improvement of about percent in the boiling A T over unmodified tubing.
The foregoing tests also establish the superiority of the 26-fin modified tube over the l9-fin modified tube, in a reduction from 5.3 F. for the l9-fin tube to 3.0 F. for the 26-fin tube.
FIG. 12 graphically illustrates the enhancement in boiling which follows bending or forming the fins of a 26-fin tube, such as seen in FIG. 1, to the form shown in FIG. 3. In this tube, where the gap between the crests of the fins and the side surface of the adjacent fin convolution has an average dimension of 0.002 0.045 inch. From this graph, it will be noted that at 6 feet per ton, the boiling AT for 26-fin standard tube is 12 F. The finned tubing modified in accordance with the present invention is referred to as Z-fin tube, and for the 26 Z-fin tube illustrated in FIG. 3, the boiling AT is 2.5 F. for an improvement of about percent in the boiling film temperature drop. 7
FIG. 5 illustrates another fin configuration for a single helix tube when formed by a process other than drawing through a circular die. In this Figure no attempt is made to illustrate a gap between the crest portion of a finned convolution and the side of the next adjacent convolution, but it is to be understood that an average gap of less than 0.007 inch will be provided.
Referring now to FIG. 6 there is illustrated a modified finned tube 24 produced from a double or twostart fin. In this case each of the fins 26 is inclined towards each other so that a gap of controlled dimensions is provided at 28 between the crests of the fins. With this arrangement a helical substantially enclosed space or chamber 29 is formed.
In FIG. 7 the fins30 are bent toward each other in such a way as to define a gap 32 therebetween, this gap appearing between spaced apart fin portions which are relatively flat in cross-section. With this configuration it will be apparent that the confined space 34 is essentially smaller than the space 29 provided between the fins in FIG. 6.
In FIG. 8 an arrangement is illustrated in which one of the fins 36 is not modified and the other fin 38 is bent towards the unmodified fin as illustrated so as to produce the helical substantially enclosed space or chamber 40 and the controlled restricted gap or opening 42. j
Referring now to FIG. 9 there is illustrated an arrangement generally similar to that shown in FIG. 6 except that the separate fins 44 and 46 are curved and inclined towards each other to produce a substantially circular cross-section enclosed space or chamber 48 and the narrow restricted gap 50.
The tubing of FIGS. and 11 is produced from finned tubing have three interleaved helical fins. In FIG. 10 the fins 62 and 64 are illustrated as bent toward the intermediate unmodified fin 63 so as to define the substantially enclosed spaces or chambers 66.
In FIG. 11 the fins, here designated 62a and 64a, are bent in a different manner toward the intermediate fin 63a to define the substantially enclosed spaces or chambers 66a.
It will be understood that in the embodiments of the invention illustrated in FIGS. 6 to 11, the modification of the normally outwardly or radially extending fins is provided progressively along the helical paths occupied by the fins. For this reason the simple embodiment of the invention illustrated in FIGS. 2-5 is preferred, since the fins are given the required configuration by the simple act of drawing the finned tube through the appropriate circular die.
While the present disclosure is broadly applicable to enhancement of boiling in any liquid, it is particularly advantageous in the art of refrigeration, where the boiling or vaporization is of a refrigerant.
The finned tube as illustrated in FIG. 1, prior to bending over the fins, has in a typical example the following dimensions: The internal diameter of the tube is 0.557 inch and the wall thickness, measured from the inside of the tube to the bottom of the space between adjacent fins is 0.035 inch. The fins have a radial dimension of 0.057 inch and are provided at a frequency of about 26 fins per inch, giving a pitch from fin convolution to fin convolution of approximately 0.038 inch. The individual fins have a thickness at the base of approximately 0.0165 inch and at the tip or crest of 0.0075 inch. This gives an average width of approximately 0.012 inch. The space between adjacent fins increases from approximately 0.021 inch adjacent the roots of the fins to approximately 0.0305 inch adjacent the crests.
The finned tubing illustrated in FIG. 1 has an approximate outside diameter, before the bending of the fins, of 0.740 inch. The configuration illustrated in FIG. 2
results from drawing this tube through a die having an internal diameter of 0.695 inch and produces a gap 16 into the substantially enclosed space 17 of 0.0035 0.0050inch.
Theconfiguration illustrated in FIG. 3'results from drawing the tubing illustrated in FIG. 1 through a die having an internal diameter of 0.688 inch, which produced a gap 18 communicating with the space 19 of 0.002 0.004s inch.
The configuration illustrated in FIG. 4 resulted from drawing the tubing of FIG. 1 through a die having an internal diameter of 0.675 inch. In this operation the crests of each fin convolution were bent over into con tact with the next adjacent fin convolution with such force as to provide deformation of the material, as has been previously described.
The dimensions of the fins in relationship to spacing are of course of critical nature since this determines the general shape and dimensions of space which is enclosed when the outer portion of each fin convolution is bent over into close proximity to the adjacent wall portion of the adjacent fin convolution, to provide the restricted opening into the substantially enclosed space. For uniform and readily controllable conditions, the fin height should be greater than the spacing between adjacent fins and the fin tip thickness should be substantially less than the fin thickness at the root. With this configuration the fins are readily bent and can be formed to touch the adjacent fin, and at the same time enclose a substantial volumetric space with accurate control of the gap providing for ingress of liquid and egress of vapor from the substantially enclosed space.
Bending of the fins is facilitated where the height of the fin is substantially greater than the average width, as for example, not less than twice the average width.
In all cases the fins are formed by rolling up material from the outer wall of the tubing, so that the fins originally extend generally perpendicular to the surface from which they were displaced, and portions thereof extend generally parallel to corresponding portions of adjacent fin convolutions.
Since the fins are originally produced by a rolling operation, the average spacing between adjacent fin portions is greater than the average thickness of the fins. This results inherently in the production of substantially enclosed spaces or chambers, after the outer portions of the fins are bent over, which are of quite substantial size. At the same time, the openings into the substantially enclosed spaces may be very restricted, by bending the outer portions of tube convolutions into very close spacing from the side surface of adjacent fin portions.
What I claim as my invention is:
1. The method of making tubing modified for the enhancement of boiling of liquid in contact with the exterior surface thereof which comprises rolling up fin convolutions out of the material at the exterior of the tubing with each convolution extending generally radially outwardly of the tubing parallel to and spaced substantially from adjacent convolutions, and thereafter drawing the finned tube through a die having a throat with a minimum transverse dimension smaller than the outside diameter of the original fin convolutions to form the outer portions of fin convolutions completely around the finned tube into proximity to a side of adjacent fin convolutions to define therewith a substantially enclosed space extending around the tubing and a restricted opening into such space.
2. The method as defined in claim 1 which comprises using a die dimensioned to deform the outer portion of each fin convolution into solid contact with the surface of the adjacent convolution, and to provide predetermined width of the restricted opening into the space by spring-back of the outer fin convolution portion.
3. The method as defined in claim 2 which comprises using a die dimensioned to cause the outer portion of each fin convolution to deform the portion of the next adjacent fin contacted thereby as the tubing passes through the die.
4. The method as defined in claim 1 which comprises the initial step of forming the fin convolutions to extend helically around the tubing.
5. The method as defined in claim 1 in which the height of each fin prior to bending is at least twice the average thickness thereof.
6. The method as defined in claim 1 in which the average spacing between adjacent fin convolutions substantially exceeds the average thickness of each fin.
7. The method as defined in claim 5 in which the average spacing between adjacent fin convolutions substantially exceeds the average thickness of each fin.
8. The method as defined in claim 1 in which the throat of the die is dimensioned to form the outer portions of the fin convolutions into such proximity to the side of adjacent fins as to produce a gap having an average width of not more than 0.007 inch.
9. The method as defined in claim 8 in which the average width of the gap is not more than 0.005 inch.
10. The method as defined in claim 8 in which the average width of the gap is between 0.0035 0.0050 inch.
1 1. The method as defined in claim 5 in which the average width of gap is not more than 0.007 inch.
12. The method as defined in claim 5 in which the average width of gap is not more than 0.005 inch.
13. The method as defined in claim 5 in which the average width of gap is between 0.0035 0.0050 inch.
14. The method as defined in claim 6 in which the average width of gap is not more than 0.007 inch.
15. The method as defined in claim 6 in which the average width of gap is not more than 0.005 inch.
16. The method as defined in claim 6 in which the average width of gap is between 0.0035 0.0050 inch.

Claims (16)

1. The method of making tubing modified for the enhancement of boiling of liquid in contact with the exterior surface thereof which comprises rolling up fin convolutions out of the material at the exterior of the tubing with each convolution extending generally radially outwardly of the tubing parallel to and spaced substantially from adjacent convolutions, and thereafter drawing the finned tube through a die having a throat with a minimum transverse dimension smaller than the outside diameter of the original fin convolutions to form the outer portions of fin convolutions completely around the finned tube into proximity to a side of adjacent fin convolutions to define therewith a substantially enclosed space extending around the tubing and a restricted opening into such space.
2. The method as defined in claim 1 which comprises using a die dimensioned to deform the outer portion of each fin convolution into solid contact with the surface of the adjacent convolution, and to provide predetermined width of the restricted opening into the space by spring-back of the outer fin convolution portion.
3. The method as defined in claim 2 which comprises using a die dimensioned to cause the outer portion of each fin convolution to deform the portion of the next adjacent fin contacted thereby as the tubing passes through the die.
4. The method as defined in claim 1 which comprises the initial step of forming the fin convolutions to extend helically around the tubing.
5. The method as defined in claim 1 in which the height of each fin prior to bending is at least twice the average thickness thereof.
6. The method as defined in claim 1 in which the average spacing between adjacent fin convolutions substantially exceeds the average thickness of each fin.
7. The method as defined in claim 5 in which the average spacing between adjacent fin convolutions substantially exceeds the average thickness of each fin.
8. The method as defined in claim 1 in which the throat of the die is dimensioned to form the outer portions of the fin convolutions into such proximity to the side of adjacent fins as to produce a gap having an average width of not more than 0.007 inch.
9. The method as defined in claim 8 in which the average width of the gap is not more than 0.005 inch.
10. The method as defined in claim 8 in which the average width of the gap is between 0.0035 - 0.0050 inch.
11. The method as defined in claim 5 in which the average width of gap is not more than 0.007 inch.
12. The method as defined in claim 5 in which the average width of gap is not more than 0.005 inch.
13. The method as defined in claim 5 in which the average width of gap is between 0.0035 - 0.0050 inch.
14. The method as defined in claim 6 in which the average width of gap is not more than 0.007 inch.
15. The method as defined in claim 6 in which the average width of gap is not more than 0.005 inch.
16. The method as defined in claim 6 in which the average width of gap is between 0.0035 - 0.0050 inch.
US00154312A 1971-06-18 1971-06-18 Method of modifying a finned tube for boiling enhancement Expired - Lifetime US3768290A (en)

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Cited By (48)

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US3881342A (en) * 1972-07-14 1975-05-06 Universal Oil Prod Co Method of making integral finned tube for submerged boiling applications having special o.d. and/or i.d. enhancement
US3906604A (en) * 1974-02-01 1975-09-23 Hitachi Cable Method of forming heat transmissive wall surface
US4004441A (en) * 1975-08-28 1977-01-25 Grumman Aerospace Corporation Process for modifying capillary grooves
US4018264A (en) * 1975-04-28 1977-04-19 Borg-Warner Corporation Boiling heat transfer surface and method
US4059147A (en) * 1972-07-14 1977-11-22 Universal Oil Products Company Integral finned tube for submerged boiling applications having special O.D. and/or I.D. enhancement
FR2397615A1 (en) * 1977-07-13 1979-02-09 Carrier Corp HEAT TRANSFER SURFACE AND METHOD FOR MANUFACTURING THIS SURFACE
DE2758526A1 (en) * 1977-12-28 1979-07-05 Wieland Werke Ag FIBER TUBE AND THE METHOD AND DEVICE FOR THE PRODUCTION THEREOF
DE2758527A1 (en) * 1977-12-28 1979-07-05 Wieland Werke Ag FIBER TUBE AND THE METHOD AND DEVICE FOR THE PRODUCTION THEREOF
US4166498A (en) * 1976-07-13 1979-09-04 Hitachi, Ltd. Vapor-condensing, heat-transfer wall
US4168618A (en) * 1978-01-26 1979-09-25 Wieland-Werke Aktiengesellschaft Y and T-finned tubes and methods and apparatus for their making
US4179911A (en) * 1977-08-09 1979-12-25 Wieland-Werke Aktiengesellschaft Y and T-finned tubes and methods and apparatus for their making
US4186063A (en) * 1977-11-01 1980-01-29 Borg-Warner Corporation Boiling heat transfer surface, method of preparing same and method of boiling
US4195688A (en) * 1975-01-13 1980-04-01 Hitachi, Ltd. Heat-transfer wall for condensation and method of manufacturing the same
US4216826A (en) * 1977-02-25 1980-08-12 Furukawa Metals Co., Ltd. Heat transfer tube for use in boiling type heat exchangers and method of producing the same
US4258783A (en) * 1977-11-01 1981-03-31 Borg-Warner Corporation Boiling heat transfer surface, method of preparing same and method of boiling
US4313248A (en) * 1977-02-25 1982-02-02 Fukurawa Metals Co., Ltd. Method of producing heat transfer tube for use in boiling type heat exchangers
EP0057941A2 (en) * 1981-02-11 1982-08-18 Noranda Inc. Heat transfer boiling surface
US4353234A (en) * 1977-07-13 1982-10-12 Carrier Corporation Heat transfer surface and method of manufacture
DE3333822A1 (en) * 1982-09-22 1984-03-22 Hitachi, Ltd., Tokyo METHOD FOR PRODUCING A HEAT PIPE
US4438807A (en) * 1981-07-02 1984-03-27 Carrier Corporation High performance heat transfer tube
EP0161391A2 (en) * 1984-05-11 1985-11-21 Hitachi, Ltd. Heat transfer wall
US4561497A (en) * 1982-12-17 1985-12-31 Hitachi, Ltd. Heat transfer surface and manufacturing method for same
US4660630A (en) * 1985-06-12 1987-04-28 Wolverine Tube, Inc. Heat transfer tube having internal ridges, and method of making same
US4678029A (en) * 1983-09-19 1987-07-07 Hitachi Cable, Ltd. Evaporating heat transfer wall
US5018573A (en) * 1989-12-18 1991-05-28 Carrier Corporation Method for manufacturing a high efficiency heat transfer surface and the surface so manufactured
US5054548A (en) * 1990-10-24 1991-10-08 Carrier Corporation High performance heat transfer surface for high pressure refrigerants
US5146979A (en) * 1987-08-05 1992-09-15 Carrier Corporation Enhanced heat transfer surface and apparatus and method of manufacture
US5222299A (en) * 1987-08-05 1993-06-29 Carrier Corporation Enhanced heat transfer surface and apparatus and method of manufacture
US5333682A (en) * 1993-09-13 1994-08-02 Carrier Corporation Heat exchanger tube
US5415225A (en) * 1993-12-15 1995-05-16 Olin Corporation Heat exchange tube with embossed enhancement
US5896660A (en) * 1994-03-23 1999-04-27 High Performance Tube, Inc. Method of manufacturing an evaporator tube
US6067712A (en) * 1993-12-15 2000-05-30 Olin Corporation Heat exchange tube with embossed enhancement
US6382311B1 (en) 1999-03-09 2002-05-07 American Standard International Inc. Nucleate boiling surface
US6427767B1 (en) 1997-02-26 2002-08-06 American Standard International Inc. Nucleate boiling surface
DE10150999A1 (en) * 2001-10-16 2003-04-30 Peak Werkstoff Gmbh Method of profiling the outer peripheral surface of cylinder liners
US20060075772A1 (en) * 2004-10-12 2006-04-13 Petur Thors Heat transfer tubes, including methods of fabrication and use thereof
US20060075773A1 (en) * 2002-04-19 2006-04-13 Petur Thors Heat transfer tubes, including methods of fabrication and use thereof
US20070151715A1 (en) * 2005-12-13 2007-07-05 Hao Yunyu A flooded type evaporating heat-exchange copper tube for an electrical refrigeration unit
US7276046B1 (en) * 2002-11-18 2007-10-02 Biosynergy, Inc. Liquid conductive cooling/heating device and method of use
US20080196876A1 (en) * 2007-01-15 2008-08-21 Wolverine Tube, Inc. Finned tube for condensation and evaporation
US20080236803A1 (en) * 2007-03-27 2008-10-02 Wolverine Tube, Inc. Finned tube with indentations
US20090121367A1 (en) * 2007-11-13 2009-05-14 Lundgreen James M Heat exchanger for removal of condensate from a steam dispersion system
US20090166018A1 (en) * 2007-11-13 2009-07-02 Lundgreen James M Heat transfer system including tubing with nucleation boiling sites
US20090260792A1 (en) * 2008-04-16 2009-10-22 Wolverine Tube, Inc. Tube with fins having wings
US20110226457A1 (en) * 2010-03-18 2011-09-22 Golden Dragon Precise Copper Tube Group Inc. Condensation enhancement heat transfer pipe
US10088180B2 (en) 2013-11-26 2018-10-02 Dri-Steem Corporation Steam dispersion system
US10174960B2 (en) 2015-09-23 2019-01-08 Dri-Steem Corporation Steam dispersion system
CN109737646A (en) * 2019-03-07 2019-05-10 常州九洲创胜特种铜业有限公司 Evaporation tube and its application and preparation method

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Cited By (69)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3881342A (en) * 1972-07-14 1975-05-06 Universal Oil Prod Co Method of making integral finned tube for submerged boiling applications having special o.d. and/or i.d. enhancement
US4059147A (en) * 1972-07-14 1977-11-22 Universal Oil Products Company Integral finned tube for submerged boiling applications having special O.D. and/or I.D. enhancement
US3906604A (en) * 1974-02-01 1975-09-23 Hitachi Cable Method of forming heat transmissive wall surface
US4195688A (en) * 1975-01-13 1980-04-01 Hitachi, Ltd. Heat-transfer wall for condensation and method of manufacturing the same
US4018264A (en) * 1975-04-28 1977-04-19 Borg-Warner Corporation Boiling heat transfer surface and method
US4004441A (en) * 1975-08-28 1977-01-25 Grumman Aerospace Corporation Process for modifying capillary grooves
US4166498A (en) * 1976-07-13 1979-09-04 Hitachi, Ltd. Vapor-condensing, heat-transfer wall
US4313248A (en) * 1977-02-25 1982-02-02 Fukurawa Metals Co., Ltd. Method of producing heat transfer tube for use in boiling type heat exchangers
US4216826A (en) * 1977-02-25 1980-08-12 Furukawa Metals Co., Ltd. Heat transfer tube for use in boiling type heat exchangers and method of producing the same
US4353234A (en) * 1977-07-13 1982-10-12 Carrier Corporation Heat transfer surface and method of manufacture
US4159739A (en) * 1977-07-13 1979-07-03 Carrier Corporation Heat transfer surface and method of manufacture
FR2397615A1 (en) * 1977-07-13 1979-02-09 Carrier Corp HEAT TRANSFER SURFACE AND METHOD FOR MANUFACTURING THIS SURFACE
US4179911A (en) * 1977-08-09 1979-12-25 Wieland-Werke Aktiengesellschaft Y and T-finned tubes and methods and apparatus for their making
US4258783A (en) * 1977-11-01 1981-03-31 Borg-Warner Corporation Boiling heat transfer surface, method of preparing same and method of boiling
US4186063A (en) * 1977-11-01 1980-01-29 Borg-Warner Corporation Boiling heat transfer surface, method of preparing same and method of boiling
DE2758527A1 (en) * 1977-12-28 1979-07-05 Wieland Werke Ag FIBER TUBE AND THE METHOD AND DEVICE FOR THE PRODUCTION THEREOF
FR2413625A1 (en) * 1977-12-28 1979-07-27 Wieland Werke Ag FINNED TUBE FOR HEAT EXCHANGERS
DE2758526A1 (en) * 1977-12-28 1979-07-05 Wieland Werke Ag FIBER TUBE AND THE METHOD AND DEVICE FOR THE PRODUCTION THEREOF
US4168618A (en) * 1978-01-26 1979-09-25 Wieland-Werke Aktiengesellschaft Y and T-finned tubes and methods and apparatus for their making
EP0057941A2 (en) * 1981-02-11 1982-08-18 Noranda Inc. Heat transfer boiling surface
EP0057941A3 (en) * 1981-02-11 1982-12-08 Noranda Inc. Heat transfer boiling surface
US4438807A (en) * 1981-07-02 1984-03-27 Carrier Corporation High performance heat transfer tube
DE3333822A1 (en) * 1982-09-22 1984-03-22 Hitachi, Ltd., Tokyo METHOD FOR PRODUCING A HEAT PIPE
US4561497A (en) * 1982-12-17 1985-12-31 Hitachi, Ltd. Heat transfer surface and manufacturing method for same
US4678029A (en) * 1983-09-19 1987-07-07 Hitachi Cable, Ltd. Evaporating heat transfer wall
EP0161391A2 (en) * 1984-05-11 1985-11-21 Hitachi, Ltd. Heat transfer wall
EP0161391A3 (en) * 1984-05-11 1986-10-22 Hitachi, Ltd. Heat transfer wall
US4660630A (en) * 1985-06-12 1987-04-28 Wolverine Tube, Inc. Heat transfer tube having internal ridges, and method of making same
US5146979A (en) * 1987-08-05 1992-09-15 Carrier Corporation Enhanced heat transfer surface and apparatus and method of manufacture
US5222299A (en) * 1987-08-05 1993-06-29 Carrier Corporation Enhanced heat transfer surface and apparatus and method of manufacture
US5018573A (en) * 1989-12-18 1991-05-28 Carrier Corporation Method for manufacturing a high efficiency heat transfer surface and the surface so manufactured
US5054548A (en) * 1990-10-24 1991-10-08 Carrier Corporation High performance heat transfer surface for high pressure refrigerants
EP0483047A1 (en) * 1990-10-24 1992-04-29 Carrier Corporation High performance heat transfer surface for high pressure refrigerants
US5333682A (en) * 1993-09-13 1994-08-02 Carrier Corporation Heat exchanger tube
US5415225A (en) * 1993-12-15 1995-05-16 Olin Corporation Heat exchange tube with embossed enhancement
US6067712A (en) * 1993-12-15 2000-05-30 Olin Corporation Heat exchange tube with embossed enhancement
US5896660A (en) * 1994-03-23 1999-04-27 High Performance Tube, Inc. Method of manufacturing an evaporator tube
US6427767B1 (en) 1997-02-26 2002-08-06 American Standard International Inc. Nucleate boiling surface
US6382311B1 (en) 1999-03-09 2002-05-07 American Standard International Inc. Nucleate boiling surface
DE10150999A1 (en) * 2001-10-16 2003-04-30 Peak Werkstoff Gmbh Method of profiling the outer peripheral surface of cylinder liners
DE10150999C2 (en) * 2001-10-16 2003-08-07 Peak Werkstoff Gmbh Method of profiling the outer peripheral surface of cylinder liners
US6748655B2 (en) 2001-10-16 2004-06-15 Peak Werkstoff Gmbh Method for profiling the outer circumferential face of cylinder liners
US20060075773A1 (en) * 2002-04-19 2006-04-13 Petur Thors Heat transfer tubes, including methods of fabrication and use thereof
US7178361B2 (en) * 2002-04-19 2007-02-20 Wolverine Tube, Inc. Heat transfer tubes, including methods of fabrication and use thereof
US7276046B1 (en) * 2002-11-18 2007-10-02 Biosynergy, Inc. Liquid conductive cooling/heating device and method of use
US7254964B2 (en) * 2004-10-12 2007-08-14 Wolverine Tube, Inc. Heat transfer tubes, including methods of fabrication and use thereof
US20060075772A1 (en) * 2004-10-12 2006-04-13 Petur Thors Heat transfer tubes, including methods of fabrication and use thereof
US7841391B2 (en) * 2005-12-13 2010-11-30 Golden Dragon Precise Copper Tube Group, Inc. Flooded type evaporating heat-exchange copper tube for an electrical refrigeration unit
US20070151715A1 (en) * 2005-12-13 2007-07-05 Hao Yunyu A flooded type evaporating heat-exchange copper tube for an electrical refrigeration unit
US20080196876A1 (en) * 2007-01-15 2008-08-21 Wolverine Tube, Inc. Finned tube for condensation and evaporation
US8162039B2 (en) 2007-01-15 2012-04-24 Wolverine Tube, Inc. Finned tube for condensation and evaporation
US20080236803A1 (en) * 2007-03-27 2008-10-02 Wolverine Tube, Inc. Finned tube with indentations
US20090166018A1 (en) * 2007-11-13 2009-07-02 Lundgreen James M Heat transfer system including tubing with nucleation boiling sites
US9459055B2 (en) 2007-11-13 2016-10-04 Dri-Steem Corporation Heat transfer system including tubing with nucleation boiling sites
US10634373B2 (en) 2007-11-13 2020-04-28 Dri-Steem Corporation Heat exchanger for removal of condensate from a steam dispersion system
US9841200B2 (en) 2007-11-13 2017-12-12 Dri-Steem Corporation Heat exchanger for removal of condensate from a steam dispersion system
US20090121367A1 (en) * 2007-11-13 2009-05-14 Lundgreen James M Heat exchanger for removal of condensate from a steam dispersion system
US8505497B2 (en) 2007-11-13 2013-08-13 Dri-Steem Corporation Heat transfer system including tubing with nucleation boiling sites
US8534645B2 (en) 2007-11-13 2013-09-17 Dri-Steem Corporation Heat exchanger for removal of condensate from a steam dispersion system
US8641021B2 (en) 2007-11-13 2014-02-04 Dri-Steem Corporation Heat exchanger for removal of condensate from a steam dispersion system
US9194595B2 (en) 2007-11-13 2015-11-24 Dri-Steem Corporation Heat exchanger for removal of condensate from a steam dispersion system
WO2009128824A1 (en) * 2008-04-16 2009-10-22 Wolverine Tube, Inc. Tube with fins having wings
US9844807B2 (en) 2008-04-16 2017-12-19 Wieland-Werke Ag Tube with fins having wings
US20090260792A1 (en) * 2008-04-16 2009-10-22 Wolverine Tube, Inc. Tube with fins having wings
US9683791B2 (en) * 2010-03-18 2017-06-20 Golden Dragon Precise Copper Tube Group Inc. Condensation enhancement heat transfer pipe
US20110226457A1 (en) * 2010-03-18 2011-09-22 Golden Dragon Precise Copper Tube Group Inc. Condensation enhancement heat transfer pipe
US10088180B2 (en) 2013-11-26 2018-10-02 Dri-Steem Corporation Steam dispersion system
US10174960B2 (en) 2015-09-23 2019-01-08 Dri-Steem Corporation Steam dispersion system
CN109737646A (en) * 2019-03-07 2019-05-10 常州九洲创胜特种铜业有限公司 Evaporation tube and its application and preparation method

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Owner name: WOLVERINE TUBE, INC., 2100 MARKET STREET, N.E., DE

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